Emulsion treater



S. A. WILSON EMULSION TREATER Oct. 20, 1953 5 Sheets-Sheet l Filed July 28, 1947 INVENTOR. S A WILSON Oct. 20, 1953 s. A. wlLsoN EMULSION TREATER 5 Sheets-Sheet 2 Filed July 28, 1947 55 INVENTOR.

.5. A. WILSON Q M. ,wvuiqf' Oct. 20, 1953 s. A. WILSON 2,656,006

EMULSION TREATER Filed July 28, 1947 3 Sheets-Sheet 3 INVENTOR.

5. A. WILSON Cm. M

Patented Oct. 20, 1953 UNITED EMULSION TREATER Samuel A. Wilson, Tulsa,

Okla., assigner to Maloney-Crawford Tank & Manufacturing Company, Tulsa, Okla., a corporation of Dela- Ware Application July 28, 1947, Serial No. 764,136

(Cl. 18S- 2.7)

6 Claims.

This invention relates to improvements in the treatment of oil, gas and water emulsions and more particularly, but not by way of limitation, to the treatment of immiscible fluids from oil wells.

The oil and gas produced from most production stratas are usually filled with salt water which becomes intermixed with the oil and gas to provide an emulsion of oil, gas and water. The presence of the salt water in the production of oil and gas necessarily requires treatment of the emulsion to separate the emulsion coming from the well into the individual constituents.

The present invention is generally concerned with the treatment of oil, gas and water emulsions by the use of a horizontally disposed treater which provides for a longer travel and scrubbing action of the emulsion through a series of inverted trays disposed in a heated chamber for efciently and expeditiously breaking up the emulsions, and particularly emulsions that cannot be separated by the usual and conventional treaters utilized today.

It is an important object of this invention to provide an improved method and means of separating fluids and liquids of various grades and types of emulsion `iiowing from oil wells wherein the emulsion is subjected to a considerably longer travel in its flow through the treater to assure a complete scrubbing action for breaking up of the emulsion.

And still another object of this invention is to provide an improved means for treating and separating emulsions of various types flowing from oil wells wherein the emulsion is subjected to a primary step for separating the free-water, and then is directed in its flow through a series of inverted superimposed spaced trays to provide a longer scrubbing action in the separation of the clean oil therefrom.

And still another object of this invention is to provide a horizontally disposed treater for oil, water and gas emulsions flowing from oil wells that is readily portable by mounting on a truck, and which decreases considerably set-up time by elimination of upending or vertical disposition of the treater.

An additional object of this invention is to provide a horizontally disposed treater for oil well emulsions which is readily accessible to the operators, thereby saving considerable labor in servicing and maintenance as well as hook-up time and repair.

And another object of this invention isto provide a horizontally disposed treater for oil well -one side of the shell 2.

2 emulsions which is easy to insulate and thereby provide proper covering in cold weather.

And still another object of this invention is to provide a horizontally disposed treater for oil well emulsions which is economical to manufacture, durable and efficient in its operation, and wherein control apparatus provides for the proper oil-water interface in the primary and secondary stages of separation at all times.

And still another object of this invention is to provide an improved method and means for treating and separating the emulsion of various types flowing from oil wells wherein the sepa-V rated oil is stabilized to obtain the highest gravity possible under conditions of heating and washing through a prolonged travel.

And still another object of this invention is to provide a horizontally disposed treater for oil well emulsions wherein the oil-water interface is controlled in order to maintain a proper relationship between the oil-water interface at all times.

Other objects and advantages of the invention will be evident from the following detailed description read in conjunction with the accompanying drawings which illustrate my invention.

In the drawings: Figure 1 is an elevational view from one side of the treater constructed in accordance with the preferred embodiment of the invention,

Figure 2 is a vertical sectional view of the treater shown in Figure l.

Figure 3 is an end elevational view.

Figure 4 is an elevational view taken from one side of the Siphon box.

Figure 5 is a sectional elevational view taken on lines 5-5 of Figure 4.

Figure 6 is a sectional view taken on lines 6 6 of Figure 2.

Figure 7 is a sectional view taken on lines l-l of Figure 8.

Figure 8 is a plan view of the trays shown in Figure 2.

Figure 9 is a detailed view showing a modified inlet for the emulsion.

Referring to the drawings in detail, reference character 2 designates a cylindrical tank having dome shaped closure end members 4 and 6 respectively. The cylindrical tank 2 is adapted to be horizontally disposed on ya skid member 8. The tank 2 is supported on the skid 8 by a plurality of curved support members I0 secured to the skid El. As clearly shown in Figure 3, a heat exchanger l2 is horizontally disposed adjacent The exchanger l2 is 3 4 maintained in position through welded brackets A Weir box 3l is secured to one side of the I4, An inlet conduit I6 for the input of oil, wabaflle plate 2l at a point in the upper portion of ter and gas emulsion coming from the well comthe chamber 28. The Weir box 3l is open at the municates with the exchanger. The exchanger top to permit the spilling or discharge of the oil can be of any suitable type causing ow through 5 and water emulsion in the chamber 2i! into the one side of the heat exchanger, and then reversbox 3|. The Weir box 3i communicates with a ing itself k(not shown) ina counterflow'charged plurality: off-conduits 32 extending` through the from the-he`at`exc`hanger V'I2 into an outlet co'nbalile'r plate 2l.: As clearly shownin' Fig-ure 6,

duit II communicating with a cylindrical tank three conduits 32 are preferably utilized, but it is or flume I8 vertically disposed in relationship to'* 10-"t0, be understood that the invention is not limited the horizontal shell 2. As clearly shown in yEigthereto: 'Ifhe conduits 32 provide communicaure 2 the tank member I8 extends through-fan tionitfror'rthe lower portion of the box 3i, and a aperture I9 of the shell 2 and i s p artial lyjdis lowentray' member @3f-disposed in the chamber posed in the interior of thejshell 2.? The-'upper'A 29 f'theliorizontally disposed shell 2. The tray portion of the tank I8 extends' aboveiandffex'- Yl5 member-33fishdisposed adjacent the bottom of teriorly of the shell 2. A mist extractor 2U is disthe tank 2 but isfsupported in spaced relation posed in the upper portion of the tank I The thereto by, end bra ckets 33.

dome 2I of the tank or ume I8 is'povidedlwitli' Referring' to'Figres 2, 6, '7 and 8, it will be a gas outlet 22, as will be hereinafter referred to." apparn'tlthat the tray section in the shell 2 com- The emulsion of oil, gas and water discharging 2O prises a plurality or series of trays 313, 35 and 36 from the heat exchanger i2, and through -the dispersed abovethe lower trayf andin vertical conduit I'I flows from the open end '2 3' of conduitvr Slllfdllatml 50 @i-h Qth THQ trays re in- A I'I and into the vertical tankv I8 at a point subterconnected with each otherby supporting bars; stantflly below the surface 5 of the emulsion 35 and 33 crnfnunicats with an immedt-l-Y present inaJ chamber 28j. 25 upper tray 3d through a conduitilfand'tray 3ft Ifhe influent discharging'into the Hume I8 will communicatesivith anirnmediately u pp-ertray535- i' flow downward into the free-water knock-out thrqugh conduit 33,- whi1e tray ,35 comrnunicates compartment 23 to immediately extract the freewith atray Serthrough Yconduit 39. JAn outlet`- watertherefrom'.' The gas entrained in the in Da SS'agev/ ay liiion thetoppxsltly llomllin'ifluent rnixtureland discharging into the flume 30 cateskwith thechainber '29.7j therewith, due ie ite-lighter derisityw'iu rise iReferringie Figures? arida'it"wi1l`be`htedl` thrlcughfand above the emulsion mixture, and that*each. ofgthe-trays.comprises a substantially flow i nto the mist extractor 2i! disposed in the rectangularly shaped bodyportion disposed in the] upperportion of the vflume I 8, The gasflowing Shell 2in an inverted position, as shown inv''iugure" up'wardinto the extractor 20 will be stripped of 35 7. j fjachof thetray membersis" providedwth it'liduid constituents, are permitted to lcngitudinallyextendmg bam@ lllcltes lill'and 22.7 owdownward tlfirough pipe Zf'jbagk A'intoY the The ballefil is secured t o an endfiof the trayinunt emulsion; The" separated lighter con- While bailei. is secured-to partially transverse st iuterigs Win pass v01jthr'ugl; the gas- Outlets baite member 45 arrangedini-spaced relation to 22. The disposition ofthe inlet pipe I 'I and the 43 thewendportionl of thetraig Eurthermore, theV 01dzv-23s-$uch as t0 DGIIYI? the Separationbeflle plates @land 2donot-extendthe complete of the free-'water prior to the separation ofthe lengthojf the tray, butare Vterrniated adjacent"V gijfmfthe emulsion mXtulfe. l The gaseous the opposite end portions to provide a 'passage-l vapors rising through -the 'emulsion mixture in Way fQllfeVClSngthf? IQW of the emulsion there? irr'rlje @will hai/ea tendenqyto 'be stripped of .i5 thlmlghi aS-Willbe hrsnaftr--sei .f OftH- Th theieliquid constituents through Contact ofthe presentinvention;*discloses 1only ourgtrays, but gaseous vapors rising upward through liquids at tgwllnbe understood that itis not limited therea Very slow Velocity.- to, and an'ynumber of traysdependent upon the? @mail and Wai-,e1- emision s pumg' .or djg.-Y size and diametervof'the-tank-E Amaybe' utilied chargingrrgmihe renderen ini@ the rhirrie le -50 if desired; o. flows downward to pass out the open lowervend As clearly shown in Figures'l and 2, the shell 2f 24 thereof. The rank is, at 'iisiewerendis pre- 1 iS plm/ide@ with a furnavrheater-@S `disposed vided with a circumferential flange Y25,jpreferalfyly 'UTaQSVCISely-'Il-he clfiarnberv VV2 9l ofY .the shell'fprovided with a plurality .ofperforatiorig 25, The heater l mayutilizeeither gas-or oil-for- As clearly shown in Figure 2, 't he horizontallyy 'applying-heeft() the'chambr-'S A Vertical flue"` disposed shelrg isprovidedwith a'baliie plate 2'I memberA'I-extends from the heater d5. l The flue -f welded to the inner peripheryand-providing Vthe llllbrrY eupprted br-"brackets 8-welded ito-n chamberg at one 4end of theta-nk balledgorsepathe shell- Thetransverse y disposition of the;V rated from a larger chamber 29, as will-be 'here-` 11331311546- is -n-pr0Ximty of the baeplate -2'1-, f inafter referred tg; The Chambgrgais prilfr'afbly 60 however, the heat from the furnace maintains'jv knowhes." the 'free-water (chamber, in ihatthe the Watereinthe-Chamber'reat afsubstantially emulsionspilling from the-numeri@ will dep'ogii; even oriconstant-temperature' throughout the Y all free-water included therewith, and will ilowjv Chamber duf- @0f-a GheI-mQ-SYDhQDC @0151011 Crlfupward through and aroundthe perforated Bange by?? 110W' 9f thefumulio .through th Series 0f 25 migo the upper half portonpf the hamber 23; '65 superimposed spaced trays, as will be hereinafter- Any lighter gasbubbles inf the oil and water emul- Set ,fglfthsieriiriii riseie the ser-ieee arieihreak eut of the The eiiand water emulsii'i liews from the Weir emulsion and discharge through a conduit '29 Y box 3Ij through the conduits 32-'into the chamber communicating with a conduit/ 3d in-turn com- 48-offthe 10wer tray-SS Iandf'hence through-one munica'ting with the tankor ilur'rle i8 for'directside-'offth'e'finverte --tr v t ingthefilow fof the gas bubbles' into lthe"m`ist"U70 flow is-reversedbgthexibvlepeprlntiirgit extraererfze therein; I1: will' ihushe apparent counter-flow urti-1 it is again 'reversed vbythe that/theseparated gases' intheemulsioninthee baiiie Illl. The emulsion is then dischargedt chamber' '28' ^are discharged directly to the mistv throughgthe-outlet conduit 3'! to an immediateh7 extractor' 26.' 75 uppertray- 3ftA where fthe-operation repeated' through the series of super-imposed spaced trays. The emulsion after passing through the series of trays is discharged through an outlet 4D. During the flow of the emulsion through the series of trays, it is broken up, due to the scrubbing action of the long travel, and the application of heat from the furnace 46 to the salt water inthe chamber 29. As is well known, the usual oil and water emulsion comprises a plurality of globules of salt water entrained in films of oil. The long travel of the emulsion plus the application of the heat from the furnace 46 causes the entrained salt water in the globules to distort, thereby breaking up the emulsion. This reaction is also activated by the fact that the application of heat will reduce the surface tension of the oil lm to assist in breaking up of the emulsion as is well known in the treating of emulsion of this type. During the travel of the emulsion through the series of trays, the water breaking out therefrom is discharged from an inverted tray onto the top of the immediate lower tray, and into the chamber 29. It will be apparent that water breaking out of the emulsion is precluded from again coming in Contact with the emulsion travel, due to the inverted disposition of the trays providing the fiat top portion 49 as clearly shown in Figures 2 and 8. The oil broken from the emulsion globules will continue to travel therewith, and is discharged from the outlet 40 as substantially clean oil. The oil from outlet 49 is disposed above the toprnost tray 35 and is permitted to discharge through the outlet conduit 5l). The conduit 59 is disposed transversely in the tank 2 at an angle to the horizontal (Figure 3) and communicates with the heat exchanger i2 (Fig. 3) in order that the heated clean oil flowing from the shell 2 to the heat exchanger may be utilized for heating emulsion from the well, and at the same time cool the outlet oil from the treater. The clean oil passes from the heat exchanger to an outlet pipe (not shown) to disposal such as a tank farm.

The pre-heating of the incoming emulsion has the advantage of assisting in the removal of the free-water therefrom, as the emulsion discharges from the flume I8 into the free-water knock-out compartment in the lowermost portion of chamber 28. Furthermore, the cooling of the clean oil in the outgoing stream prevents evaporation losses in the storage tanks.

The amount of free-water in the lower portion of the chamber 28 is controlled by the amount or layer of the oil and water emulsion disposed thereupon, as the oil and water emulsion discharges from the chamber I3 and through the perforated flange 25. The pressure of the oil and water emulsion against the lower layer of freewater causes the free-water to discharge through a pipe 5| communicating between the shell 2 and a siphon box 52, Figure 3. The siphon box cornprises a cylindrical tank member 52, vertically disposed at one side of the cylindrical tank 2, and supported in one instance by the conduit 5I. The pipe 5I is welded at its entrance to the shell 2 for maintaining the box 52 in the substantially vertical upright position. The box 52 is disposed exteriorly of the shell 2 in a line substantially parallel to that of the baille plate 2l' so that the conduit 5I provides communication between the box 52 and the chamber 28, as clearly shown in Figure A similar pipe or conduit 55 assists in supporting the box 52, and also provides communication between the box 52 and the chamber 29 on the opposite of the baffle plate 21 (Fig. l). The bottom portion of the siphon box 52 is provided with a plurality of apertures 54 and 55 around which are welded threaded couplings 56 and 51 in cornmunication with the pipes 5| and 53 respectively. A short nipple 59 is adapted to be received in the coupling 55, while a longer nipple 69 is threaded into the coupling 51. Free-water in the chamber 28 ilows through the pipe 5l and nipple 59 into the box 52, while in similar manner the scrubbing water broken from the emulsion in chamber 29 is caused to flow through the connecting conduit 53 and nipple 50 into the siphon box 52. An outlet aperture 6l permits discharge of the water ilowing into the siphon box to any conventional disposal means (not shown).

The length of the nipples 59 and 89 is important in controlling the height of the oil emulsion being treated in the shell 2 and particularly in the chambers 28 and 29. A proper oil-water interface must be maintained in the chamber 29 through the complete travel of the emulsion in the series of trays, and particularly to the top of the uppermost tray 35. The height of the nipple 60 of a pre-determined length determines this in the following manner: It will be apparent that if the height of the nipple 55 were decreased it would change the hydrostatic head in the chamber 29 and thereby lower the oil-water interface to decrease the emulsion travel in the top tray 36. In such a condition the top tray 36 would contain substantially clean oil broken from the emulsion and would not include any salt water necessary in the scrubbing action in the travel through the top tray 36. Similarly any decrease in height or length of the nipple 59 would'lower the emulsion and free-water interface in chamber 28 to decrease the salt water scrubbing action in the free-water knockout compartment, thereby substantially lessening the reaction of the free-water removal from the flume I8.

As the scrubbed and clean oilbroken from the emulsion passes from the upper outlet 49, the lighter gases that may be in solution will break out and rise to the surface, and hence flow from the shell 2 through the outlet conduit 35 providing communication through the shell and the flume i8. This gas from the clean oil is usually at high temperature and upon reaching the cool mist extractor will condense and cause any trapped oil therein to fall by gravity into the emulsion flowing from the open end of the pipe 23 in the fiume I8. The upper portion of the siphon box 52 is connected with a pipe 52 which in turn connects with the equalizing pipe 39 communicating with the oil and gas separator tank I8. The conduit 62 precludes any siphonic action on the water discharging from the outlet 5| by equalizwater from the outlet 5l and stop the operation Y of the treater. Similarly the conduit equalizes the pressure between the chamber 29 and the shell 2 and the upper portion of the flume I8 containing the mist extractor 25 in order that the flow of gas and liquids between these chambers will be maintained.

As clearly shown in Figure 2, the emulsion is stratied in both chambers 28 and 29 wherein the heavier dash lines in the lower portion of the chambers represent the extracted water, and the medium dash lines represent the oil and Water emulsion disposed thereabove, `while the lighter dash lines in the upper part of the Vchambers represent lthez gaseous :vapors liberated: from'ian'd risi-n'glabove the'- emulsi'o'ngi. The' scrubbi'ng'iyvater1"i in'i'th'e'ch'amber 29.'isusually accumulatedffromfs.'

theflow of -th'elemulsion' from the Weirlbox howev'er'; it will be apparent that thescrubb'ing water maybe eitheraccumulated or disposed-therein,"

creases-f the temperature of the scrubbing Water'. inlproximity of the furnace, causing it to rise, and Y consequentlyth'e Water at a lower temperature infv` proximitykof fthe' tankrendr will displace' theris-A ing* 'water and. create a l substantialtliermosy-Jy phonicflow in the chamber 29.

The thermo-syphonic action is not created by anyf'recirculation of the precipitated water in'rthe chamb'er-Zglbut-'is due'mainly to the disposition" of the heater flat one rend of the chamber-29.`V

In-Figure 9 is shown a modified form of-th'e in'` ventionl-fwherein'the inlet pipe 12f isl disposed fin,"

suchfa mannerasrto'provide communication from-` tlieexchanger l2'to an upper portion ofthe flume I8?? The inlet'l2; at its outlet end (not shown) isl` disposed immediately below the mist extractor 202i- In this manner the ree gases or lighter' gaseous-vapors in the innuent emulsion mixture discharging into-the nume v 8 are primarily liberated ratusifor the treatment of oil, *gas` and water emulsions, Wherein'tlie emulsion mixture is pro-v Vid'ed withl a prolonged travel through-a series of horizontally' disposed; trays arranged in an elongated scrubbing chamber ofA a horizontally dis-v posedvshell member. The prolonged travel through the elongated horizontal path lwill eie'ctV a'breaking .upof oil, Water and gas emulsionsfin a more eflicient 'and positive manner-,@andfparticularly emulsions which are" normallydifiicult to' break up. The emulsion mixture flows' inthe Y prolonged horizontalpath, and' the 'precipitated Wat'er extracted therefrom is bailedo or pre-- clu'ded from. coming in contact with the oWingemulsion', once it is extracted. Furthermore, rthe presentinvention contemplates a nov'el'controlvv apparatus communicating withv both .the free'- waterandv Lthe scrubbingv chambers, ord'er to'v maintaina proper oil-water interface #relation-1f. shipinboth 'the chambers at "all-'tiines-x The lighter-"gaseous constituents rising from-the stratiedloilinlthefreelwater ch'amber,`or fromthe Y clean oil in the scrubbing chamber are"V permitted and into direct contact with the mistfextractor'- Without'passage through any other chamber.Vv

Changes may be made in the specifications-and drawings withoutdeparting from the spirit of the invention within the scope of the following claims,

asset forth. Y

What'I claim' is z Liman-emulsion treating apparatus comprisinging-horizontally disposed shell having a plurality of separate chambers therein comprising a freewaterextraction chamber and an elongated scrubbing chamber, said scrubbing chambervbe-l ing"Y disposed horizontally, a vertically disposed iiumamounted on the shell and having an open lower 'endcommunicating with the vinterior of thefex'traction chamben'gas separating means inVV theniiumegraninuent inlet disposed below the sepa-ratingffmeans, means forrdirecting thevinfluentfrdownwa'rdly through the flume'to beY dis-1 8 charged-into the: free-water:- extractingl chamberf passage, means for conducting the f emulsion-rupe ward 1fromthe-nume' forstratication above the-f:l extracted water, me'anslfor conductingliberated- `gasesiromthe upwardly rising emulsion tothe* .vide a tortuous path-"of the emulsion flowing thereto, and means-for carrying off the scrubbed oil from the uppermost of said trays.

2J In an oilv emulsion treater comprising a horif-r zontally disposed shell hav-ing a Afree-water eX-" "tracting chamber, a ume-having an open end."

in communication withy thechamber, an iniiuent: mixture inlet'communicating with the nume-and disposed below the level of the emulsion' mixture in -thev chamber, means' forfstratifying the emul` sionmixture in the chamber, means conduct-ing the stratified emulsion from-the-iree-water chambber'to a horizontal heated scrubbing chamber, a plurality of horizontally extended 'superimposedff trays arranged in inverted position l andV disposed.A in the scrubbing chamber, said -f' traysVV in "com-A munioation with theconducting means,`-a plu'=- rality-loaxially disposed bailles" provided inthe' trays toprovide a tortuouslpath of thev emulsion-l iio'wing therethrough, A said 1 inverted position "of the' trays-preventing scrubbed water falling froma tray from' contacting the o'wing emulsion; and'` outlet means for the separated oil.

v3.5m an emulsion treating apparatus compris'' inga closed horizontally' disposed'l shell, a nume mounted on the shell' and communicating"'there`` with,; an emulsion inlet'fin the iiumefan :oil outlet in "the fshell, heating means inthe shell to assist inbreakingthe emulsion, a primary chamber* infth shell for extracting free-water from' the 'emulsion-a separate horizontally disposed scrubbingchamber including the heating means,` a plurality offsupe'rimposed trays adapted` to exf' tend-'in an=elongateddhorizontal path 4vand having f their l end l"portions disposed substantially pere' pendicular to the longitudinal axis ofthersh'ell', saidlftrays farranged #in an inverted position to.

provide-a at top portion-and an open'bottom""V portion, a plurality of baiiies carried by thetrays means =providing communication Abetween the in:v iiuentl'emulsion and the trays to dischargetheYA emulsion Ythrough the trays in a tortuous path, outlet-means for the separated clean oil, and outletlmeans for the precipitated water. v

4. In' an'emulsion treating apparatus compris'- ing aclosedfh'orizontally Vdisposed shellI a 'nume mounted onthe shell and communicating therewith, an emulsion inlet inthe flume; and oil out` let 'in the shell, heating 'means inthe shell'to assist `in breaking the emulsionya primary cham= ber in the'shell for extracting free-Water `fromo. the emulsion, a separateVY horizontally?` disposed scrubbing chamberV including the heating means, a plurality of superimposed trays'adapted toextend'in a substantiallyhorizontal path and havy ing their end portions disposed substantially perpendicular to thelongitudinal axis of the shell,` saidtrays arrangedin an inverted position to` provide-a -iiat topy portionand an open bottom portion,A apluralityl'of -rbales carried by the trays;

Y means providing communication betweenthe in;

nuent emulsion and the trays to direct the emulsion in a counterlowing path, means for separating the clean oil from the trays, outlet means for the precipitated water, and control means communicating with the precipitated water in the shell to regulated the oil-water interface therein.

5. In combination with an oil Well emulsion treater, a horizontally disposed shell having a primary free-water extracting chamber, a horizontal scrubbing chamber baflled therefrom, an upright tank mounted on the shell and communicating with the interior thereof, a mist extractor disposed in the upper portion of the tank, an influent mixture inlet communicating with the tank at 'a point below the surface of the water in the extracting chamber, a circular perforated piate disposed adjacent the lower end of the tank providing for discharge of the influent upwardly therethrough for stratication above the extracted free-water, means for conducting liberated gases from the upwardly rising emulsion to the mist extractor, a weir box provided in the primary chamber permitting spilling of the emulsion thereinto, a conduit providing communication between the Weir box and the scrubbing chamber, heating means in the scrubbing chamber, a plurality of superimposed communicating trays disposed in the scrubbing chamber and in communication with the conduit, said trays horizontally arranged to denne end portions substantially perpendicular to the longitudinal axis of the shell, and arranged in an inverted position to provide a flat top portion and an open bottom portion, means in the trays to provide a counterflow of the emulsion flowing therethrough, said at top portion precluding contact of the precipitated Water with the incoming emulsion, means for carrying oi the scrubbed oil, means for carrying oil the liberated gases from the scrubbed oil, and means communicating with the precipitated water in the shell to control the oil-water interface therein.

6. In an oil emulsion treater comprising a horizontally disposed shell having a free-water extracting chamber, a nume having an open end in communication therewith, a mist extractor in the flume, an inuent inlet disposed in the upper portion of the flume below the mist extractor to provide for discharge of gaseous vapors from the inlet mixture to the mist extractor, means conducting the stratified emulsion from the freewater chamber to a horizontal heated scrubbing chamber, a plurality of horizontally extended superimposed trays arranged in inverted position 'and disposed in a scrubbing chamber, said trays in communication with the conducting means, a plurality of axially disposed baffles provided in the trays to provide a counterflow of the emulsion flowing therethrough, said inverted position of the trays preventing scrubbed water falling from a tray from contacting the flowing emulsion, and outlet means for the separated oil.

SAMUEL A. WILSON.

References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,648,558 Meston et al Nov. 8, 1927 1,869,758 Lungstras Aug. 2, 1932 2,167,160 Raymond July 25, 1939 2,261,057 Erwin Oct. 28, 1941 2,297,297 Walker Sept 29, 1942 2,384,222 Walker Sept. 4, 1945 2,457,959 Walker Jan. 4, 1949 2,601,904 Erwin July 1, 1952 

